Patent GB-1025509-A (GB)
Title: Method and apparatus for controlling a vapor generator operating at supercritical pressure
IPC: F01K13/02
Filed: 1964-08-14
Abstract: 1,025,509. Regulating feedwater supply to steam boilers. COMBUSTION ENGINEERING Inc. Aug. 14, 1964 [Aug. 21, 1963], No. 33327/64. Heading F4A. The feedwater supply to a once through boiler operating at supercritical pressure is regulated in accordance with load by flowing a minor proportion of the feedwater through a control tube or tubes at a rate corresponding to the load, comparing the control tube outlet temperature with a desired value for the particular load and adjusting the feedwater flow to bring the measured value into correspondence with the desired value. As shown in Fig. 1, the boiler is fed by a pump 26 through a regulator valve 50, the water flowing through an economizer 24 to the evaporator tubes 16 whence steam flows through superheaters 21, 22 and line 32 to a turbine 34. The rate of firing of the boiler by a burner 12 is adjusted according to load changes as shown by pressure changes in the line 32 measured at 42. Final steam temperature is held constant throughout the load range by feedwater injection at 53 as controlled by temperature measured at 56. A control tube or tubes 60 is arranged in parallel with the evaporator tubes 16 so as to absorb heat proportional to that absorbed by the tubes 16, the flow through the control tube being regulated by a valve 62. This valve is set according to load by a unit 78 receiving a signal from a comparing device 76, which compares a signal from a set point indicator 75 of a magnitude depending on steam flow as measured at 66 and set on a cam 73 by a device 69, with a signal from a device 57 representative of the difference in temperature of the control vapour as sensed at 65 and the temperature of the main flow entering the superheater 21 as measured at 48. Any out-of-balance is transmitted as a signal to the unit 78 which adjusts the valve 62 to the changed load in response to difference in temperature. In a modification, Fig. 5 (not shown), the positioning of valve 62 is directly related to load whilst in another modification, Fig. 4 (not shown), the valve is positioned according to the difference in flow between the feed-water supply to the tubes 16 and the supply to the control tube. The loadcontrolled device 69 also sets a cam 70 which adjusts the magnitude of a desired value impulse from a set point receiver 74 to comparing device 63. This device compares the signal with one representative of the control temperature as measured at 65 and transmits a signal representative of any out-of-balance to a unit 49 which appropriately adjusts the feed regulator valve 50 to equalize the temperature at 65 with the desired value. Thus the flow through the control tube 60 is adjusted according to the load on the boiler so that at all points in the load range variations in temperature of wide magnitude which are representative of variations of heat input are available for control, the control point is located close to the feedwater regulator in the working medium flow path so that the time lag in control response is reduced and the control temperature is not located at a too high temperature level which may necessitate excessive amounts of injection water for superheat control.